EP3145898B1 - Verfahren zur behandlung eines abfallgemisches, einschliesslich trennung und kompostierung des besagten gemisches - Google Patents

Verfahren zur behandlung eines abfallgemisches, einschliesslich trennung und kompostierung des besagten gemisches Download PDF

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Publication number
EP3145898B1
EP3145898B1 EP15732793.3A EP15732793A EP3145898B1 EP 3145898 B1 EP3145898 B1 EP 3145898B1 EP 15732793 A EP15732793 A EP 15732793A EP 3145898 B1 EP3145898 B1 EP 3145898B1
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Prior art keywords
waste
wastes
fraction
mixture
orifices
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English (en)
French (fr)
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EP3145898A1 (de
Inventor
Fabien Michel Alain CHARREYRE
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Finance Developpement Environnement Charreyre FIDEC SARL
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Finance Developpement Environnement Charreyre FIDEC SARL
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Priority to PL15732793T priority Critical patent/PL3145898T3/pl
Publication of EP3145898A1 publication Critical patent/EP3145898A1/de
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    • C—CHEMISTRY; METALLURGY
    • C05—FERTILISERS; MANUFACTURE THEREOF
    • C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
    • C05F17/00—Preparation of fertilisers characterised by biological or biochemical treatment steps, e.g. composting or fermentation
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03B—SEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
    • B03B9/00—General arrangement of separating plant, e.g. flow sheets
    • B03B9/06—General arrangement of separating plant, e.g. flow sheets specially adapted for refuse
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C1/00—Magnetic separation
    • B03C1/02—Magnetic separation acting directly on the substance being separated
    • B03C1/23—Magnetic separation acting directly on the substance being separated with material carried by oscillating fields; with material carried by travelling fields, e.g. generated by stationary magnetic coils; Eddy-current separators, e.g. sliding ramp
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
    • B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
    • B07B1/00—Sieving, screening, sifting, or sorting solid materials using networks, gratings, grids, or the like
    • B07B1/18—Drum screens
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
    • B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
    • B07B1/00—Sieving, screening, sifting, or sorting solid materials using networks, gratings, grids, or the like
    • B07B1/18—Drum screens
    • B07B1/22—Revolving drums
    • B07B1/24—Revolving drums with fixed or moving interior agitators
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
    • B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
    • B07B1/00—Sieving, screening, sifting, or sorting solid materials using networks, gratings, grids, or the like
    • B07B1/46—Constructional details of screens in general; Cleaning or heating of screens
    • B07B1/4609—Constructional details of screens in general; Cleaning or heating of screens constructional details of screening surfaces or meshes
    • B07B1/469—Perforated sheet-like material
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
    • B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
    • B07B13/00—Grading or sorting solid materials by dry methods, not otherwise provided for; Sorting articles otherwise than by indirectly controlled devices
    • B07B13/14—Details or accessories
    • B07B13/16—Feed or discharge arrangements
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
    • B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
    • C—CHEMISTRY; METALLURGY
    • C05—FERTILISERS; MANUFACTURE THEREOF
    • C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
    • C05F17/00—Preparation of fertilisers characterised by biological or biochemical treatment steps, e.g. composting or fermentation
    • C05F17/10—Addition or removal of substances other than water or air to or from the material during the treatment
    • C—CHEMISTRY; METALLURGY
    • C05—FERTILISERS; MANUFACTURE THEREOF
    • C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
    • C05F17/00—Preparation of fertilisers characterised by biological or biochemical treatment steps, e.g. composting or fermentation
    • C05F17/50—Treatments combining two or more different biological or biochemical treatments, e.g. anaerobic and aerobic treatment or vermicomposting and aerobic treatment
    • C—CHEMISTRY; METALLURGY
    • C05—FERTILISERS; MANUFACTURE THEREOF
    • C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
    • C05F17/00—Preparation of fertilisers characterised by biological or biochemical treatment steps, e.g. composting or fermentation
    • C05F17/90—Apparatus therefor
    • C05F17/964—Constructional parts, e.g. floors, covers or doors
    • C—CHEMISTRY; METALLURGY
    • C05—FERTILISERS; MANUFACTURE THEREOF
    • C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
    • C05F17/00—Preparation of fertilisers characterised by biological or biochemical treatment steps, e.g. composting or fermentation
    • C05F17/90—Apparatus therefor
    • C05F17/964—Constructional parts, e.g. floors, covers or doors
    • C05F17/971—Constructional parts, e.g. floors, covers or doors for feeding or discharging materials to be treated; for feeding or discharging other material
    • C05F17/986—Constructional parts, e.g. floors, covers or doors for feeding or discharging materials to be treated; for feeding or discharging other material the other material being liquid
    • C—CHEMISTRY; METALLURGY
    • C05—FERTILISERS; MANUFACTURE THEREOF
    • C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
    • C05F9/00—Fertilisers from household or town refuse
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
    • Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
    • Y02A40/20—Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00—Technologies for the production of fuel of non-fossil origin
    • Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/141—Feedstock
    • Y02P20/145—Feedstock the feedstock being materials of biological origin
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00—Technologies for solid waste management
    • Y02W30/40—Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00—Technologies for solid waste management
    • Y02W30/50—Reuse, recycling or recovery technologies
    • Y02W30/52—Mechanical processing of waste for the recovery of materials, e.g. crushing, shredding, separation or disassembly

Definitions

  • the present invention relates to the field of waste treatment, in particular the treatment of household waste and waste from economic activities for their recycling, their recovery, or their reprocessing.
  • the invention relates more specifically to a process for treating a mixture of waste, the latter being of heterogeneous sizes, shapes and consistencies, a non-negligible portion of the mass of the mixture of waste being formed by biodegradable waste, for example at least 10% of the mass, and a non-negligible portion of the mass of the mixture being formed by non-biodegradable recyclable waste, for example at least 10% of the mass.
  • a non-negligible quantity of waste is thus generally buried or incinerated, whereas it could be subject to composting, recycling, or transformation into solid recovered fuel.
  • a maximum of 20% of the mass of household waste is generally recycled.
  • WO-2007/098610A1 describes a method and a system for composting waste formed predominantly by organic waste from pre-sorting (SSO).
  • the objects assigned to the present invention therefore aim to remedy the various drawbacks listed above and to propose a new process treatment of a mixture of waste making it possible to recover a very large portion of the mixture of waste.
  • Another object of the invention aims to provide a new process for treating a mixture of wastes making it possible to selectively recover one or more portions of the mixture of wastes despite the heterogeneity of said mixture of wastes.
  • Another object of the invention aims to provide a new method for treating a mixture of general-purpose and universal waste, making it possible to treat any type of waste.
  • Another object of the invention aims to provide a new process for treating a mixture of waste, making it possible to generate products whose value is much higher than the initial value of the mixture of waste.
  • Another object of the invention aims to provide a new process for treating a mixture of waste that is inexpensive and easy to implement.
  • Another object of the invention aims to provide a new process for treating a mixture of waste making it possible to reduce the quantity of infrastructures for collecting and treating waste from local authorities.
  • Another object of the invention aims to propose a new process for treating a mixture of waste making it possible to simplify the organization of the collection of waste by communities, companies and households.
  • Another object of the invention is to propose a new method for treating a mixture of waste allowing treatment of the mixture of waste in a predominantly or even totally automated manner.
  • Another object of the invention is to provide a new process for treating a mixture of waste, making it possible to sort a mixture of waste on an industrial scale.
  • the invention relates as such to a process for treating a mixture of waste 2, aimed at refining, recovering and/or recycling all or part of the waste of the latter, and in particular biodegradable waste, recyclable waste, and of the combustible waste it contains.
  • the waste mixture 2 is preferably formed by household waste, but can also be formed by waste from economic or industrial activities, or both, said waste having undergone no prior sorting or grinding.
  • This mixture of waste 2 is thus advantageously formed of waste generated by households, during consumption and the daily life of the latter.
  • the mixture of waste 2 has not undergone any treatment and forms a mixture of raw waste 2.
  • no grinding of the raw waste mixture was carried out, nor any prior sorting aimed at segregating one type of waste from another, and in particular at separating biodegradable waste and recyclable waste. not biodegradable.
  • the mixture of waste 2 has been collected, for example using garbage trucks, from households and/or economic activities without said households and/or said economic activities having carried out a prior sorting or selection of the waste. collected.
  • the collection of waste mixture 2 was not selective.
  • the process of the invention is a process for treating a mixture of unground raw waste.
  • the mixture of waste 2 may on the contrary have been stripped of a portion of the recyclable waste it contains, for example by households during a pre-sorting , or have itself been pre-sorted, for example by households.
  • the waste from the mixture of waste 2 is advantageously collected in a raw and undifferentiated way, mixed in bags, of the type plastic trash bags closed by households.
  • the method comprises a step E7 of opening bags 24, of the plastic garbage bag type, in which bags 24 are contained the mixture of waste 2, in order to releasing said waste mixture 2 from said bags 24 to perform step E1.
  • This bag opening step is automated so that there is no manual processing involved.
  • the waste mixture 2 thus released from the bags 24 is preferably grouped together to form the waste mixture 2 used in the treatment process.
  • the opening of the bags 24 of waste can be carried out for example using a bag opening device, to allow the release of the waste from said bags 24, preferably without damaging or altering said waste.
  • the waste is of heterogeneous sizes, shapes and consistencies, preferably of nature and origin. varied.
  • the waste mixture 2 thus considered may in particular include both soft, hard, sharp, liquid, powdery, solid, flat, hollow, solid, sticky, slippery, greasy, brittle, flexible, compressible, incompressible, combustible, incombustible waste. or even combining several of these characteristics.
  • the mixture of waste 2 contains mostly used and undesirable elements, for example food waste, newspapers, paper, cardboard, glass, plastic, metal, textiles, various combustibles and incombustibles, complex materials , hazardous household waste, inert waste, bulky items.
  • a non-negligible portion of the mass of the mixture of waste 2 is formed by biodegradable waste, for example at least 10% of the mass, and a non-negligible portion of the mass of the mixture is formed by recyclable waste 26 non-biodegradable, for example at least 10% by mass.
  • At least 10%, preferably at least 20%, of the mass of the mixture of waste 2 is formed by biodegradable waste, and at least 10%, preferably at least 20%, of the mass of the mixture is formed by non-biodegradable recyclable waste 26.
  • biodegradable waste means waste which, under the action of a natural environment, comprising for example living organisms and/or air and/or water, can naturally and spontaneously break down into various elements likely to damage the natural environment (high oxygen demand, emission of leachate) if they have not been stabilized, for example by composting.
  • Living organisms can in particular be formed by microorganisms such as bacteria, fungi or algae, which are likely to degrade biodegradable waste using biochemical reactions.
  • biodegradable waste preferably means waste which can be degraded in this way on the time scale of a human life, of a decade, or more preferably of a year or a few months, preferably of a few weeks.
  • biodegradable waste preferably means waste capable of entering into the manufacture and formation of compost by composting the latter.
  • Non-biodegradable waste within the meaning of the invention, forms other waste, which does not spontaneously and naturally undergo such degradation, or which undergoes it too slowly. “ Non-biodegradable ” waste is in particular unsuitable for forming compost by composting the latter.
  • non-recyclable waste refers to any waste not falling within the categories described above of “ recyclable waste ” and “biodegradable waste ”.
  • non-recyclable waste includes in particular waste with a calorific value that makes it capable of being transformed into solid recovered fuels, and other unusable ultimate waste (complex waste, etc.) intended for example for landfill. or incineration.
  • the process is an industrial process in which the steps are carried out in sequence and in parallel with each other. For example, while waste undergoes a given stage, other waste simultaneously undergoes another stage.
  • the treatment method of the invention comprises a step E1 during which the mixture of waste 2 is separated into a first fraction of waste 13 whose size is less than approximately 180 mm, preferably less than 140 mm, and a second residual waste fraction 14.
  • size generally means a dimension of the space of the waste according to its longest length, or a characteristic dimension.
  • size ” of a waste means a characteristic geometric dimension of the individual waste, which allows it, for example, to pass through a mesh of corresponding size if the size of the waste is less than the size of the mesh, or on the contrary not to pass if the size of said waste is greater than the size of said mesh.
  • second residual portion of waste means the remaining portion of waste, which has not corresponded to the characteristics of separation of the first portion of waste 13, in this case the size criterion.
  • the second residual portion of waste 14 can contain waste whose size is less than 50 mm.
  • the first fraction of waste 13 is advantageously formed by waste having on average a higher density than the waste of the second residual fraction of waste 14, insofar as, in practice, the waste of density the higher are preferably of size less than 180 mm.
  • Step E1 is advantageously carried out using a sorting machine 1 described below, an embodiment of which is shown in figures 4 to 6 .
  • step E1 of the process thus includes a separation of the waste whose size is sufficiently small, whose density is the highest, whose dynamic inertia is the greatest, the most sticky, greasy waste , messy and wet from the mixture of waste 2 to form the first fraction of waste.
  • the latter is thus advantageously formed of at least a majority of waste having such properties.
  • the first fraction of waste 13 thus mainly concentrates organic and/or biodegradable waste, which most of the time has the aforementioned properties.
  • a non-negligible portion of the mass of the first fraction of waste 13 is formed by biodegradable waste, for example at least 50% of the mass of the first fraction of waste 13, or even at least 60%, or even preferably at least 80%.
  • a non-negligible portion of the mass of the second residual fraction of waste 14 is advantageously formed for its part by non-biodegradable recyclable waste, which may possibly be separated and recovered later.
  • the second residual fraction of waste 14, at the end of step E1 contains a negligible proportion of biodegradable waste.
  • a non-negligible portion of the mass of the second residual fraction of waste 14 is formed by recyclable waste, for example at least 50% of the mass of the second residual fraction of waste 14, or even at least 60%, even preferably at least 80%.
  • a non-negligible portion, but as small as possible, of the mass of the first fraction of waste 13 is advantageously formed for its part by biodegradable waste, which can be separated and subsequently recovered in a simplified manner.
  • less than 40% of the mass of the second residual fraction of waste 14 is formed at this stage from biodegradable waste, preferably less than 25%, or even less than 10%.
  • the first fraction of waste 13 and the second residual fraction of waste 14 can be treated more easily in the following steps of the process, in particular insofar as the waste of the second residual fraction of waste 14 are, at this stage, cleaned of most of the organic and/or biodegradable, sticky, messy and nauseous waste.
  • the waste from the first fraction of waste 13 has a size of less than about 110 mm, and is separated using a sorting machine 1 including for example a rotary trommel, as described below.
  • a sorting machine 1 including for example a rotary trommel, as described below.
  • the method comprises, at the end of step E1 or simultaneously with the latter, a step E4 of separating the second residual fraction of waste 14 into a sub-fraction of large waste and a sub-fraction of small waste 15, the large waste sub-fraction being formed by waste whose size is greater than the small waste sub-fraction 15.
  • the large waste sub-fraction is preferably formed by waste whose size is greater than about 330 mm, the sub-fraction of small waste 15 being formed by waste whose size is less than about 330 mm.
  • Step E4 can be performed for example using a sorting machine 1 described below, with a rotating trommel.
  • waste fractions and sub-fractions 13, 15, 18 recovered separately can thus be treated independently, despite the very great heterogeneity of the initial waste 2 mixture.
  • the treatment method preferably includes a step E5 of manual sorting of the large waste sub-fraction 16, making it possible to separate on the one hand the recyclable waste 26 that it contains, and on the other hand the non-recyclable waste 27 that it contains.
  • Manual sorting is advantageously made possible at this stage, insofar as the waste is of sufficiently large size, devoid of small size waste and most of the fines.
  • the waste is advantageously devoid of most of the sticky and foul-smelling material formed by the biodegradable material, which makes manual sorting possible.
  • Manual sorting makes it possible in particular to separate the large waste sub-fraction 16 from metal waste 26A, plastic waste, large electronic waste, cardboard packaging, etc.
  • Waste recognized as being recyclable waste during manual sorting will advantageously be sent to a recycling stage W, as described below.
  • the residual waste which is not separated for recycling will advantageously be sent to a step X for the manufacture of solid recovered fuel, whether it is actually recyclable or non-recyclable.
  • the processing method comprises a step E6 of automated sorting of the sub-fraction of small waste 15, making it possible to separate on the one hand the recyclable waste 26 that it contains, and on the other hand the non-recyclable waste 27 what contains.
  • the small waste sub-fraction 15 is preferably suitable for automatic sorting, the small waste 15 being lighter to be handled for example by sorting devices.
  • Step E6 preferably includes a first sub-step E61 of separating metallic waste 26A contained in the sub-fraction of small waste 15, for example using an electromagnetic separator and/or a current separator. Foucault, so as to separate at least the majority of the metal waste 26A contained in said sub-fraction of small waste 15, the metal waste 26A forming at least the majority of recyclable waste 26.
  • the metal waste 26A can thus advantageously be extracted from the small waste sub-fraction 15, insofar as said small waste sub-fraction 15 is preferably substantially devoid of sticky biodegradable waste.
  • step E6 comprises a second sub-step E62, of separating the sub-fraction of small waste 15 into a flow of substantially flat waste and a flow of substantially voluminous waste.
  • the two streams of waste can be directed to sorting machines adapted to the morphology of the waste they contain.
  • substantially flat waste is understood to mean waste extending mainly on the surface, such as for example newspapers, papers, various plastic plates.
  • substantially flat waste advantageously also encompasses bulky waste that is sufficiently soft, or of sufficiently low mechanical strength to be able to be flattened or compacted easily, for example certain cardboard boxes.
  • substantially voluminous waste means waste which extends along three dimensions of space, which may be hollow, and which is more resistant than substantially flat waste to compaction, which is more rigid, or more solid.
  • substantially voluminous waste may include plastic or glass bottles, plastic boxes, vials and various containers.
  • This sub-step E62 is preferably carried out using a ballistic carpet separator (not shown).
  • the ballistic mat preferably has an inclination relative to the horizontal so as to form a slope, the tread being designed to provide forward movement in the direction of the rise of the slope.
  • the substantially voluminous waste is intended to roll and bounce on the ballistic carpet by gravity so as to slide down the slope in the direction of a low recovery means of the bin or conveyor type, optionally incorporating a glass trap.
  • the substantially flat waste is for its part preferentially driven up the slope by the advancing movement of the belt, towards a high recovery means, for example another conveyor, so that the substantially flat waste and the substantially voluminous waste are separated.
  • the fine particles likely to be contained in the small waste sub-fraction 15 advantageously adhere to the ballistic carpet (the latter can optionally be moistened to amplify this effect), and can advantageously be scraped and recovered using, for example, a tungsten strip scraper mounted on said belt.
  • the tread of the ballistic carpet can advantageously have properties of elasticity such as to allow the bouncing of substantially voluminous waste.
  • the ballistic carpet is preferably combined with an accelerator carpet mounted upstream, making it possible to accelerate the sub-fraction of small waste 15 so that the latter reach the ballistic carpet of the ballistic carpet separator with a predetermined speed.
  • step E6 comprises a third sub-step E63 of robotic sorting on the one hand of the stream of substantially flat waste and on the other hand of the stream of substantially voluminous waste, to separate from each of said streams recyclable waste 26 and non-recyclable waste, the third sub-step E63 being carried out at the end of the second sub-step E62.
  • separate sorting robots adapted respectively to the sorting on the one hand of substantially flat waste and on the other hand of substantially voluminous waste will be chosen.
  • the sorting robots are preferably designed to separate recyclable waste from substantially flat waste and substantially voluminous waste by recognizing these latter, in particular by optical signature recognition, in particular allowing the sorting robot to detect the material of the waste to be sorted.
  • the recyclable waste recognized by the sorting robots will advantageously be sent to a recycling step W.
  • the unrecognized waste preferably including a small proportion of recyclable waste and a majority of non-recyclable waste, will advantageously be sent to a step X for the manufacture of solid recovered fuel.
  • the recyclable waste can advantageously be the subject of a step T of the treatment process, during which non-ferrous metal waste is separated from the recyclable waste, for example using an eddy current separator.
  • the non-ferrous metal waste is for example formed by aluminum waste, or alternatively flexible food packaging containing aluminum foil.
  • the separate streams of substantially voluminous waste and substantially flat waste are conveyed using a set of belt conveyors to the sorting robots, the set of belt conveyors being designed to spread out and distribute the waste so that substantially no waste is superimposed on another when said waste arrives at the sorting robots.
  • the efficiency of sorting by the robots is thus advantageously improved.
  • the sub-steps E61, E62 and E63 are preferably carried out successively in this order.
  • the treatment method of the invention also comprises a step E2, carried out successively in step E1, during which the first fraction of waste 13 is subjected to a composting process so as to compost at least part of the waste. biodegradable it contains.
  • Step E2 thus preferably aims to recover the first fraction of waste 13, and in particular to convert the biodegradable waste it contains into a mixture of refined waste 28, so that, preferably, the mixture of waste refined 28 forms compost that meets the NF U 44-051 standard.
  • the NF U 44-051 standard of 2006 called " Organic amendments - Names, specifications and marking ", is a French standard.
  • Step E2 advantageously includes the treatment of the first fraction of waste 13 by two successive composting cycles separated by a drying step of the first fraction of waste 13 at the end of the first composting cycle to facilitate the separation and the easier refining of the first fraction of waste 13.
  • the first fraction of waste 13 is particularly heterogeneous and has many undesirables not likely to be treated by composting, it is possible to refine the latter to the using step E2 to obtain refined waste 28 whose value is greater than that of the initial waste mixture.
  • composting means a biological process for converting and recovering organic waste, and in particular the biodegradable waste contained in the first fraction of waste 13, by promoting and/or by accelerating the natural process of biodegradation.
  • the composting cycles of step E2 preferentially make it possible to convert at least a portion of the first fraction of waste 13 into a stabilized, hygienic product, rich in humic compounds, preferably into compost.
  • composting means composting, for example traditional or industrial, implementing in particular an action of microorganisms to degrade and putrefy waste from the first fraction of waste 13, these microorganisms being naturally present in the first fraction of waste 13 and/or added to the first fraction of waste 13, and/or brought to multiply in the first fraction of waste 13.
  • This composting implements in particular an aeration of the first fraction of waste 13, and/or regulating the humidity of the first fraction of waste 13 (for example by adding water to the first fraction of waste 13 and/or by reintroducing into the first fraction of waste 13 composting juice 11 emitted by the latter ), and/or an addition of microorganisms to the first fraction of waste 13 and/or an addition of structurants 17C to stimulate the composting process, and/or a supply of light, for example sola ire.
  • step A corresponds to, or comprises, a phase of degradation of the waste, in particular biodegradable
  • step C corresponds to, or comprises, a phase of maturation of the waste, in particular biodegradable, to obtain the mixture of waste refined 28, the latter advantageously forming compost.
  • the degradation phase advantageously results in a proliferation of microorganisms in the first fraction of waste 13, while the maturation phase preferentially results in the gradual decrease in the quantity of microorganisms having proliferated during the degradation phase. , and the conservation of beneficial micro-organisms for the soil.
  • the degradation and maturation phases can overlap or even be confused.
  • the first composting cycle advantageously allows the composting of the biodegradable portion of the first fraction of waste 13, while, of course, the non-biodegradable waste remains substantially unaltered, and serves in particular as structurants 17C to the composting process, structuring 17C waste being intended in particular to improve the circulation of air in the within the first fraction of waste 13 being composted, to improve the aerobic composting.
  • the first composting cycle of step A is advantageously carried out aerobically.
  • the first fraction of waste 13 to be composted is preferably aerated, in particular using the circulation of an air flow passing through the first fraction of waste 13 to be composted, or by stirring the first fraction of waste 13.
  • a 5C light source is preferably added to the first fraction of waste 13 to improve its composting, for example a natural 5C light source, and/or an artificial 5C light source.
  • the waste concerned being arranged in a pile that is turned over several times, for example using a suitable 1C loader, in order to contribute to aerating the waste (as illustrated for example in the figure 9 ).
  • the first fraction of waste 13 is placed in at least one first composting bay 3C, for example in a heap.
  • the waste from the light waste portion 13C is placed in at least one second composting bay 3C.
  • the waste concerned is moistened using sources of humidity 6C
  • the sources of humidity 6C being for example formed by watering devices or watering ramps with which the first and/or second composting bays are equipped, the piles being intended to be watered by the watering devices, the said watering devices being for example placed above the said piles .
  • Step E2 advantageously includes a step Y during which composting juices 11 oozing from the mixture of waste are recovered to supply the sources of humidity 6C.
  • step Y can also include rainwater collection to supply the humidity sources 6C, which in particular makes it possible to reduce the possible consumption of running water, in particular drinking water, of step E2.
  • the first fraction of waste 13 contains a major proportion of wet and/or sticky waste, formed in particular by biodegradable waste, or at least suitable for composting.
  • Their sticky and/or wet character advantageously facilitates their separation from the second residual fraction of waste by the sorting machine.
  • step E2 comprises a step Z during which metal waste 26A contained in the first fraction of waste 13 is separated, for example using an electromagnetic separator and / or an eddy current separator, so as to separate at least the majority of said metal waste 26A contained in the mixture of waste 2.
  • the first fraction of waste 13 intended for the first composting cycle is thus devoid of the major part metallic waste 26A that it contained, and in particular those whose size and/or mass is significant, so that the composting process of the first composting cycle is favored and accelerated.
  • the metal waste 26A thus separated in stage Z can advantageously be the subject of stage W of recycling.
  • step B carried out after step A for the first fraction of waste 13 considered, makes it possible to remove all or part of the humidity 6C from the mixture of pre-composted waste 2 during said step A.
  • the mixture of pre-composted waste 2 for example placed in a pile in at least one, if not several, drying bays, and subjected to drying.
  • Step B preferably comprises a sub-step B1 of circulating a flow of drying air A dry through said mixture of pre-composted waste 2 to dry the latter, the flow of drying air A dry crossing at this effect preferably the pile of waste from side to side.
  • the drying air A dry is advantageously formed by a current of dry air heated to a temperature of between 40° C.
  • the circulation of the drying air flow A sech takes place vertically, preferably from top to bottom, otherwise from bottom to top.
  • a suction of air 8C drying under the pile of pre-composted waste is advantageously generated.
  • step B the mixture of pre-composted waste 2 is placed in a heap in drying bays, for example on the floor of the latter.
  • step E2 comprises turning the pile over once or several times.
  • At least a portion of the moisture 6C contained in the mixture of pre-composted waste 2 is recovered during step B, and the sources of 6C humidity with the portion of the 6C humidity thus recovered.
  • the humidity 6C of the mixture of pre-composted waste 2 is thus removed from the latter during step B to then be reintroduced into the portion of light waste 13C of step D, so that this humidity is not wasted, and is reused, at least in part.
  • composting juices 11C emanating from the mixture of pre-composted waste 2 during drying are recovered, for example by draining the latter using a drainage means 9C of the drying bay 2C.
  • These composting juices 11C are advantageously stored, and transported to be reintroduced later in the implementation of first and second composting cycles.
  • the composting juices 11C comprising in particular water, micro-organisms and other elements useful for the smooth running of composting, their reintroduction via sources of humidity 6C into a mixture of waste 2 to be composted improves the composting of the latter while reducing the need to bring water, micro-organisms and other elements useful for the smooth running of the composting from the outside.
  • the drying air A dry is put into circulation at least by means of an air blow 7C carried out above the mixture of pre-composted waste 2, so that the drying air A dry drains the 6C moisture from the pre-composted waste 2 mixture, the step of recovering the moisture portion being performed at least in part by condensing the 6C moisture from the pre-composted waste 2 mixture and drained through the drying air flow A dry .
  • each drying bay 2C advantageously comprises a recuperator 10C of a portion of the humidity 6C contained in the mixture of pre-composted waste 2 during the drying of the latter, the recuperator 10C of humidity making it possible to supply the 6C moisture sources with 6C moisture recovered during the drying of said pre-composted waste.
  • the flow of drying air A dry having circulated through the mixture of pre-composted waste 2 is treated to substantially relieve it of any composting emission, in particular odorous, using for example filtering, or biochemical treatment.
  • the drying bay(s) preferably comprises means for treating the drying air A dry having circulated through the mixture of pre-composted waste 2 to discharge it substantially from any composting emission, in particular odorous .
  • the air emissions and possible pollutants linked to the implementation of step E2 are advantageously treated in this way, which allows step E2 to be substantially non-polluting and not to generate of smells.
  • said step E2 comprises a step E during which a portion of waste whose size is greater than approximately 30 mm, called 17C structuring waste, whether it is biodegradable waste or not, composted or not, and the concentration of 17C structuring waste of other waste undergoing stage A is adjusted by adding the portion of 17C structuring waste thus separated from the mixture of dried waste 2, in particular so as to structure and seed the first composting cycle.
  • the separation of the structuring waste 17C is advantageously carried out using a rotating trommel whose mesh allows the segregation of objects whose size is greater than about 30mm, and objects whose size is less than about 30mm.
  • the structuring waste 17C of the mixture of dried waste 2 is thus advantageously reused to improve a first composting cycle in progress or subsequent to other waste.
  • 17C structurants from an external source.
  • a greater or lesser portion of the 17C structuring waste recovered is advantageously reintroduced into the waste undergoing step A so as to adjust, by topping up, the concentration of 17C structuring agents in said waste up to a predetermined value, preferably specific to improve the first cycle of composting.
  • the recovered 17C structuring waste which is not reintroduced may preferably be sorted, for example manually or using a machine of the rotary trommel type, so as to separate recyclable waste, which the recycling, and non-recyclable waste, which is subjected to a step X of manufacturing solid recovered fuel (SRC), or another type of reprocessing such as landfilling or incineration.
  • SRC solid recovered fuel
  • step C all or part of the elements undesirable in the formation of the final refined waste mixture 28 are separated during step C.
  • step E2 all or part of the biodegradable waste have undergone the first cycle of composting, so as to be composted, at least in a way partial, and that this same biodegradable waste is dry, and therefore in particular non-sticky, disseminated in the form of powder or pre-compost gravel which adheres less significantly to non-biodegradable waste.
  • This pre-composted and dry biodegradable waste moreover, advantageously has, for the most part of them, a low density and distinct from the rest of the waste of the mixture of dried waste 2.
  • the portion of light waste 13C comprises a majority concentration of biodegradable waste capable of being transformed into compost. It is thus easier to make a selection of the waste likely to form the mixture of refined waste 28 from among the mixture of waste 2, which was initially relatively heterogeneous.
  • Stage C and stage E are preferably carried out using means for separating the mixture of dried waste 2 at least into a portion of heavy waste 25 and a portion of light waste 13C, the portion of heavy waste 25 being substantially formed by waste with a higher density than the waste from the light waste portion 13C.
  • the separation means advantageously also include the trommel associated with step E.
  • the trommel associated with step E may optionally be equipped with a brush making it possible to clean the portion of light waste 13C by rubbing, in order to separate the aforementioned waste.
  • the portion of light waste 13C separated during step C has a density of less than approximately 0.7 kg/L, preferably less than approximately 0.6 kg/L, the dry compost generally having a mass volume close to 0.5 kg/L.
  • Plastic materials with a density most often greater than 0.8 kg/L can thus easily be separated from the portion of 13C light waste. It is thus advantageously possible to separate from the portion of light waste 13C the plastics, including chlorinated plastics such as polyvinyl chlorides (PVC), so that the mixture of refined waste 28 will be substantially free of them at the end of the stage D, or will be provided with it in negligible proportions.
  • PVC polyvinyl chlorides
  • gravel and other stones, metals, glass, degraded or degrading paper fibers can also be separated during step C, so that the refined waste mixture 28 will be substantially free at the end of step D, or will be provided with it in negligible proportions.
  • step C preferably comprises a first sub-step C1 during which the mixture of dried waste 2 is separated from the residual metal waste 26A that it contains, for example using an electromagnetic separator and/or an eddy current separator, so as to separate at least the majority of the residual metal waste 26A contained in said mixture of dried waste 2.
  • the “dried” state of the waste advantageously facilitates such separation.
  • This first sub-step C1 preferentially contributes to the formation of a mixture of refined waste 28 of good quality, and in particular of a compost satisfying standard NF U 44-051.
  • Step E2 thus preferably comprises a step W of recycling the metal waste 26A initially contained in the first fraction of waste 13.
  • Sub-step C1 is preferably carried out before the separation of the heavy waste and the light waste.
  • Step C preferably comprises a second sub-step C2, during which the mixture of dried waste 2 is separated, in addition to the portion of heavy waste 25 and light waste 13C, into a portion of intermediate waste 19C whose density is intermediate, that is to say between the density of the waste of the first and second portions of waste, and that said portion of intermediate waste 19C is added to waste undergoing stage A.
  • Intermediate waste 19C whose density is for example greater than approximately 0.6 kg/L but less than approximately 0.7 kg/L, are preferably returned to a first composting cycle in accordance with step A. Indeed, it is possible that intermediate 19C waste can be formed by biodegradable waste whose degradation of the first composting cycle would be incomplete, or whose drying would be incomplete.
  • This second sub-step C2 thus makes it possible to improve the separation between the waste which will enter into the composition of the mixture of refined waste 28, and the other waste.
  • the second sub-step C2 is preferably carried out after the sub-step C1, and contributes to the separation of heavy waste and light waste.
  • Step C, the first sub-step C1 and the second sub-step C2 are advantageously carried out at least using the aforementioned separation means, comprising in particular a ballistic carpet separator 12C (as illustrated for example in figures 7 and 8 ) and an associated densimetric table separator.
  • step E2 preferably implements a first ballistic carpet 12A making it possible to first separate the portion of heavy waste 25, the rest of the mixture of dried waste 2 being directed towards a second ballistic carpet 12B making it possible to separate a portion of light waste 13C and a portion of indeterminate waste 15C.
  • the portion of indeterminate waste is advantageously directed towards the densimetric separator, which makes it possible to separate the portion of indeterminate waste more finely, in particular by separating light waste joining the portion of light waste 13C, heavy waste joining the portion of heavy waste 25 , and the portion of intermediate waste 19C described above.
  • the first and the second ballistic carpet 12A, 12B are preferably included in the same machine, as illustrated in the figures, the first ballistic carpet 12A directly feeding the second ballistic carpet 12B by gravity.
  • An accelerator mat can advantageously be placed upstream of the first ballistic mat 12A so as to accelerate the mixture of dried waste 2 to project them onto the first ballistic mat 12B with a certain kinetic energy capable of improving the separation of the waste.
  • the first ballistic mat 12A and the second ballistic mat 12B preferably have an inclination in the longitudinal direction, which inclination is adjustable, for example between 20° and 70° with respect to the horizontal, in order to make it possible to adjust the separation of the waste. .
  • the first and/or the second ballistic carpet 12A, 12B preferably comprises an elastic tread making it possible to bounce and roll certain types of waste on said tread (in particular the most massive of them ), some other waste being intended on the contrary to adhere to the tread.
  • the tread may moreover advantageously have adherent or sticky properties, in particular for making the finest waste.
  • the mixture of dried waste 2 comprises in particular fines, which can be advantageously recovered to be introduced into the portion of light waste 13C, for example by scraping the ballistic mats 12C using a tungsten scraper fitted to said ballistic mats (not shown).
  • stage E2 preferably comprises a stage F during which the portion of light waste 13C is separated, a portion of 18C coarse waste whose size exceeds 12 mm, for example using a rotating trommel whose mesh allows the segregation of objects whose size is greater than about 12 mm, and objects whose size is less than about 12 mm.
  • the coarse waste 18C forms, in this case, light waste whose size is too large to be able to enter into the composition of the mixture of refined waste 28, and in particular to form compost complying with standard NF U 44-051. All or part of this portion of coarse waste 18C is advantageously crushed to be reintroduced into the portion of light waste 13C during step D.
  • all or part of this portion of coarse waste 18C is preferentially reintroduced into waste undergoing stage A.
  • all or part of this portion of coarse waste 18C which may be formed from non-compostable waste, may enter stage X for the manufacture of solid recovered fuel, or be the subject, if possible, of step W of recycling.
  • step D preferably makes it possible to refine the decomposition of the organic waste contained in the first fraction of initial waste 13 .
  • the second composting cycle is carried out on the portion of light waste 13C, which comes from the first fraction of waste 13, which has been deprived of the vast majority, if not all of the waste not conforming to the formation of the final refined waste mixture 28.
  • a mixture of refined waste 28 of good quality, and capable of meeting particular standards, is thus obtained.
  • the end of step E2 most, if not all, of the biodegradable waste the first fraction of waste 13 enters into the composition of the mixture of final refined waste 28 .
  • Step D is preferably carried out by placing the portion of light waste 13C, for example in a heap, in at least one second composting bay 3C, for example similar to the first composting bay 3C.
  • Stage D advantageously comprises at least one sub-stage D1 of rewetting the light waste, for example with the 6C humidity recovered during stage B of drying, in order to promote natural composting, and in particular the maturation of the compost during the second composting cycle to form the refined waste mixture 28.
  • stage D also includes aeration of the light waste, for example similar to stage A (using a flux of air, or several reversals of the pile of light waste) to promote the formation of refined waste 28.
  • Stage D can also preferably comprise the reintroduction of microorganisms into said light waste, coming for example from the first composting cycle of stage A.
  • the treatment method comprises a step W during which recycling of non-biodegradable recyclable waste 26 which has previously been separated from the first waste fraction 13 during step E2 and recyclable waste 26 that one has previously separated from the second residual fraction of waste 14, for example during steps E4, E5 or E6.
  • step E2 preferably makes it possible, during its progress, to extract and separate recyclable waste 26 from the first fraction of waste 13, just like steps E4 to E6.
  • the portion of heavy waste 25 is added to the second residual fraction of waste 14 at the end of step E1, in particular to undergo step E4 and/or steps E5 and/or E6 described above, in the measure where they advantageously comprise a majority proportion of non-biodegradable recyclable waste compared to the proportion of biodegradable waste.
  • the treatment method advantageously further comprises a step X during which waste, preferably non-recyclable waste, which has been separated from the first fraction of waste 13 is subjected to a solid recovery fuel manufacturing process. during step E2 and which has been separated from the second residual fraction of waste 14, for example during step E6.
  • the waste thus recovered preferably non-recyclable and not recoverable in other sectors (recycling or manufacture of compost), is advantageously substantially devoid of chlorinated elements, so that they can be used in the manufacture of solid recovered fuel. Indeed, most of the chlorinated elements, for example waste containing PVC, have preferably been separated beforehand during stages of the treatment process.
  • Stage X advantageously includes a sub-stage for separating the fines from the non-recyclable waste, so as not to convert waste devoid of fines into solid recovery fuel.
  • Step X advantageously comprises a sub-step of selection of waste having a calorific value above a predetermined threshold, in order to manufacture solid recovered fuel whose calorific value is particularly high.
  • Stage X preferably comprises a sub-stage during which high calorific value elements are added to the waste from stage X, said high calorific value elements being separate from the waste from the treatment process, in order to increase , or to regulate the calorific value of the solid recovered fuel.
  • Stage X advantageously comprises a sub-stage of adding ordinary industrial waste to the waste from stage X.
  • the fines recovered from the waste during the steps described above can either enter step E2 for the production of compost, or be destroyed or buried.
  • waste that could not be recycled, transformed into compost or solid recovered fuel is preferentially buried or incinerated.
  • the invention also relates as such to an installation for processing a mixture of waste 2, the latter being of heterogeneous sizes, shapes and consistencies, a non-negligible portion of the mass of the mixture of waste 2 being formed by biodegradable waste, for example at least 10% of the mass, and a non-negligible portion of the mass of the mixture being formed by non-biodegradable recyclable waste 26, for example at least 10% of the mass.
  • the installation described below preferably makes it possible to implement the treatment process described above, and preferably forms a waste treatment and sorting plant.
  • the treatment installation of the invention comprises a rotary sorting machine 1, making it possible to separate the mixture of waste 2 into a first fraction of waste 13 and a second residual fraction of waste 14, the first fraction of waste 13 whose size is less than about 180 mm, preferably less than 140 mm.
  • the vocation of the sorting machine 1 is advantageously to organize the waste of said mixture of waste 2, by classifying and separating the waste it contains by categories according to their nature or specific characteristics.
  • the waste thus sorted by the sorting machine 1 can in this way advantageously be the subject of the treatments described above, which could not be carried out when said waste is in the state of the initial mixture of waste 2.
  • the sorting machine 1 advantageously comprises at least a first trommel section 3, provided with a first separating wall 5 extending over a first axial length L1 and being provided with a first series of separating orifices 7, 8 crossings making it possible to separate the mixture of waste 2 into a first fraction of waste 13 crossing said first separation wall 5 via the first series of separation orifices 7, 8 and into a second residual fraction of waste 14, the waste mixture 2 being intended to circulate along said first wall in order to be thus separated.
  • the first trommel section 3 is designed to receive within it the mixture of waste 2 to carry out a first sorting of the latter.
  • said first section of trommel 3 is provided to bring the mixture of waste 2 into contact with the first separating wall 5.
  • the mixture of waste 2 is screened, and/or filtered, said first wall of separation 5 being porous, so as to allow the passage through itself of the first fraction of waste 13, and to prohibit the passage through itself of the second residual fraction of waste 14.
  • the first waste fraction 13 is formed by waste whose size is smaller, on average, than that of the second residual waste fraction 14.
  • the separation orifices 7, 8 of the first series of separation orifices 7, 8 are made through the first separation wall 5, so as to make it porous, and are calibrated to let pass through them even exclusively the first fraction of waste 13, the elements of which are finer than those of the second residual fraction of waste 14, like a sieve.
  • the waste mixture 2 is intended to progress, for example by gravity, along the first separation wall 5 over the entire first length L1.
  • the latter advantageously represents the porous length of the first separation wall 5, that is to say the useful length pierced by the first series of separation orifices 7, 8.
  • the first fraction of waste 13 is evacuated from the first section of trommel 3 using for example gravity, in a first hopper 12 placed below the first section of trommel 3.
  • the second residual fraction of waste 14 remains advantageously channeled within the first trommel section 3, and is caused to pass into the second trommel section 4.
  • the first trommel section 3 preferentially makes it possible to separate therefrom the waste whose size is the smallest, whose density is the highest, whose dynamic inertia is the greatest, the most sticky, greasy, messy and wet waste of the mixture of waste 2.
  • the first fraction of waste 13 is thus advantageously mainly formed by waste having such properties.
  • the first fraction of waste 13 thus mainly concentrates organic and/or biodegradable waste, which most of the time has the aforementioned properties.
  • the first series of separation orifices 7, 8 comprises at least primary orifices 7 making it possible at least to contribute to separating the mixture of waste 2 according to the first fraction of waste 13 and according to the second residual fraction of waste 14 by passing the first fraction of waste 13 through said primary orifices 7, the latter being of a size adapted to prevent the passage of waste of a size greater than 80 mm.
  • the primary orifices 7, in this preferential case only waste small enough to form the first fraction of waste 13.
  • the size of the primary orifices 7 thus chosen preferably makes it possible to carry out a selection of good quality of the biodegradable waste, that is to say that it makes it possible to obtain a high concentration of biodegradable waste in the first fraction of waste 13.
  • the primary orifices 7 are preferably of circular section, and 'a diameter between 85 mm and 95 mm, preferably about 90 mm. It should be carefully considered that, in particular to adapt to the composition of the mixture of waste 2, other sizes and shapes of primary orifices 7 could be envisaged without departing from the scope of the invention, for example polygonal, oblong, smaller size, or larger size.
  • the primary orifices 7 are advantageously distributed evenly, so as to form a mesh, over the majority of the surface of the first separating wall 5.
  • the first series of separation orifices 7, 8 also comprises secondary orifices 8 making it possible to contribute to separating the mixture of waste 2 according to the first fraction of waste 13 and according to the second residual fraction of waste 14 by passing the first fraction of waste 13 through said secondary orifices 8, the latter being of a size adapted to allow the passage of waste whose size is between 1 times and 1.5 times the size of the waste whose passage is authorized by the primary orifices 7, the secondary orifices 8 being arranged upstream of the primary orifices 7, in consideration of the direction of circulation of the waste mixture 2.
  • the first separating wall 5 advantageously has a decreasing porosity along its first length L1, so that the waste mixture 2 is first brought into contact with the secondary orifices 8, then with the primary orifices 7, the size of the secondary orifices 8 being greater than the size of the primary orifices 7.
  • the secondary orifices 8 are preferably of circular section, and of a diameter comprised between 105 mm and 115 mm, preferably about 110 mm. It should be carefully considered that, in particular to adapt to the composition of the mixture of waste 2, other sizes and shapes of secondary orifices 8 could be envisaged without departing from the scope of the invention, for example polygonal, oblong, smaller size, or larger size.
  • the secondary orifices 8 are preferably distributed evenly, so as to form a mesh, over a minor portion of the surface of the first separating wall 5 which is unoccupied by the primary orifices 7.
  • the secondary orifices 8 are advantageously distributed over approximately one eighth of the first length L1, the secondary orifices occupying substantially the entire remaining length.
  • the secondary orifices 8 make it possible to include in the first fraction of waste 13 only a portion of waste of a size greater than that authorized by the primary orifices 7 and contained in the mixture of waste 2.
  • such a design makes it possible to ensure that the second residual fraction of waste 14 contains a lower proportion, or even substantially zero, of biodegradable waste, even if a larger portion of non-biodegradable waste is likely to be introduced into the first fraction of waste 13.
  • the sorting machine 1 also comprises a second trommel section 4, provided with a second dividing wall 6 extending over a second axial length L2, said second dividing wall 6 being provided with a second series of through separation orifices 9 making it possible to separate the second residual fraction of waste 14 into a sub-fraction of small waste 15 passing through said second separation wall 6 via said second series of separation orifices 9 and into a sub-fraction residual large waste fraction 16, the large waste sub-fraction 16 being formed by waste whose size is greater than the small waste sub-fraction 15, the second residual waste fraction 14 being intended to circulate along said second wall to be thus separated.
  • a second trommel section 4 provided with a second dividing wall 6 extending over a second axial length L2
  • said second dividing wall 6 being provided with a second series of through separation orifices 9 making it possible to separate the second residual fraction of waste 14 into a sub-fraction of small waste 15 passing through said second separation wall 6 via said second series of separation orifices 9 and into a sub-fraction
  • the second section of trommel 4 is designed to receive within it the second residual fraction of waste 14, coming from the first section of trommel 3, to carry out a second sorting of said second residual fraction of waste 14.
  • the second section of trommel 4 is preferably provided to bring the second residual fraction of waste 14 into contact with the second separating wall 6. In contact with the latter, the second residual fraction of waste 14 is screened and/or filtered, said second separating wall 6 being porous, so as to allow passage through itself of the sub-fraction of small waste 15, and to prohibit the passage through itself of the sub-fraction of large waste 16.
  • the separation orifices 9 of the second series of separation orifices 9 are provided through the second separation wall 6, so as to make it porous, and are calibrated to let pass through them even exclusively the sub- fraction of small waste 15, the elements of which are finer than those of the sub-fraction of large waste 16, like a sieve.
  • the second residual fraction of waste 14 is intended to progress, for example by gravity, along the second separation wall 6 over the entire second length L2.
  • the latter advantageously represents the pore length of the second separation wall 6, that is to say the useful length pierced by the second series of separation orifices 9.
  • the small waste sub-fraction 15 is evacuated from the second trommel section 4 with the aid of gravity, for example, into a second hopper 17 placed below the second trommel section 4.
  • the large sub-fraction waste 16 preferentially remains channeled within the second section of trommel 4 and evacuated from the latter.
  • the second trommel section 4 has for this purpose a refusal outlet through which the large waste sub-fraction 16 is intended to leave said second trommel section 4.
  • the refusal outlet 21 advantageously opens towards an evacuation hopper 18 connected to the end of the second trommel section 4, and into which the large waste sub-fraction 16 falls by gravity.
  • the second residual fraction of waste 14 is preferably substantially devoid of biodegradable, messy, sticky and/or high-density waste, which has been discarded by the first section of trommel 3, the second section of trommel 4 preferentially allows to carry out a sorting of waste, including in particular recyclable waste, present in the second residual fraction of waste 14. It makes it possible in particular, preferably, to isolate waste of relatively large size contained in the large subsection biodegradable waste 16, which could for example be manually sorted, recyclable waste and non-recyclable waste.
  • the smaller waste advantageously contained in the small waste sub-section 15 may for their part be the subject of automated sorting aimed at separating the biodegradable waste, the recyclable waste and the non-recyclable waste.
  • the subsequent sorting carried out on the small waste sub-section 15 and on the large waste sub-section 16 is advantageously facilitated, insofar as the waste is, at this stage, substantially cleaned of organic waste. and/or biodegradable, sticky, messy and foul smelling.
  • the second series of separation orifices 9 comprises at least tertiary orifices 9 making it possible at least to contribute to separating the second residual fraction of waste 14 according to the sub-fraction of small waste 15 and according to the sub-fraction large waste 16 by passage of the sub-fraction of small waste 15 through said tertiary orifices 9, the latter being of a size adapted to prevent the passage of waste of a size greater than at least 200 mm, or even 300 mm .
  • tertiary orifices 9 are thus authorized to pass through the tertiary orifices 9, in this preferential case, only waste small enough to form the sub-fraction of small waste 15.
  • the size of the tertiary orifices 9 thus chosen preferably makes it possible to carry out a selection of a predetermined type of recyclable waste, that is to say that it makes it possible to obtain a high concentration of this particular type of recyclable waste the sub-fraction of small waste 15.
  • the tertiary orifices 9 are advantageously of oblong section, and said oblong section having a small diameter Dp, and a large diameter Dg, as illustrated in particular in figure 6 .
  • the expression “ oblong section ” preferably includes a section shape, for example rectangular or elliptical, or a shape combining the characteristics of the latter.
  • the large diameter Dg and the small diameter Dp are chosen so that they correspond to the types of waste which it is desired to include in particular in the sub-fraction of small waste 15.
  • the mixture of waste 2 being capable of containing plastic or glass bottles, the standard size of which is generally about thirty centimeters, it is possible to choose a large diameter Dg of a size slightly greater than the size of said bottles, that is to say say slightly more than about thirty centimeters.
  • the mixture of waste 2 being likely to contain used newspapers, the standard size of which is generally about twenty centimeters, it is possible to choose a small diameter Dp of a size slightly greater than the size of said newspapers , that is to say slightly more than about twenty centimeters.
  • the small diameter Dp is between 200 and 240 mm, preferably around 220 mm, the large diameter Dg being between 300 and 400 mm, preferably around 330 mm, the small diameter Dp being substantially perpendicular to the large diameter Dg, as illustrated in particular in the figure 6 .
  • the composition of the initial waste mixture 2 in particular to adapt to the composition of the initial waste mixture 2, other sizes and shapes of tertiary orifices 9 could be envisaged without departing from the scope of the invention, for example polygonal, circular, smaller size , or larger size.
  • the large diameter Dg of the tertiary orifices 9 is parallel to a second longitudinal axis Y-Y' of the second trommel 4, as described below.
  • the large diameter Dg of the tertiary orifices 9 is perpendicular to the second longitudinal axis Y-Y'.
  • the tertiary orifices 9 are thus preferably substantially perpendicular to each other, so as to anticipate the orientation of the waste to be included in the sub-fraction of small waste 15, and to improve the sorting efficiency of the second trommel section 4.
  • the second series of separation orifices 9 will be formed by alternating longitudinal rows 19 and transverse rows 20 of tertiary orifices 9.
  • the first series of separation orifices 7, 8 is distributed substantially over the entire first length L1 of the first trommel section 3
  • the second series of separation orifices 9 is distributed substantially over the entire second length L2 of the second trommel section 4, so as to be distributed over at least the majority of, or even over all, the surface formed by the first dividing wall 5 and by the second dividing wall 6.
  • Such a design makes it possible to increase the proportion useful of said partition walls, and thus improve the compactness of the sorting machine 1 in general.
  • the second length L2 is less than the first length L1.
  • the first trommel section 3, and in particular the first dividing wall 5 is of a greater length than that of the second trommel section 4, and in particular the second dividing wall 6.
  • the first length L1 is advantageously chosen to be long enough so that all the waste of the mixture of waste 2 likely to pass through the first separation wall 5 are actually included in the first fraction of waste 13.
  • the first length L1 is at least 1.05 times the second length L2, preferably at least 1.10 times, even more preferably at least 1.12 times.
  • the sum of the first length L1 and the second length L2 is advantageously between 10 and 20 m.
  • the sorting machine 1 is preferably designed to sort between 10 and 50 T/h of waste mixture (2).
  • the first dividing wall 5 has the general shape of a prism, cylinder or truncated cone, the height of which forms a first longitudinal axis XX' of the first dividing wall 5, the latter being rotated about the first axis longitudinal X-X'.
  • the second dividing wall 6 has the general shape of a prism, cylinder or truncated cone, the height of which forms a second longitudinal axis YY' of the second dividing wall 6, the latter being rotated around of the second longitudinal axis Y-Y'.
  • the first longitudinal axis XX' and/or the second longitudinal axis YY' are preferably slightly inclined with respect to the horizontal, so as to allow, by gravity, a progression of the waste in the trommel sections according to a predetermined direction of circulation, advantageously from the admission inlet 10, towards the second trommel section 4, to the evacuation hopper 18 at the refusal outlet of the second trommel section 4.
  • the rotation of the first trommel section 3 and/or the second trommel section 4 allows the waste to be stirred and turned over, so that at least a majority of it, if not all of it, has the possibility of come into contact with the first dividing wall 5 and/or the second dividing wall 6 to be sorted.
  • the first trommel section 3 and/or the second trommel section 4 are each designed to be rotated, the rotation taking place preferably alternately in one direction and in the other according to a desired frequency, around their respective longitudinal axes.
  • a prismatic shape with an octagonal base to cause a rebound of the waste on the walls, in order to allow better separation of the waste from each other.
  • the diameter of the first trommel section 3 and of the second trommel section 4 is advantageously between 2 and 3 m.
  • the first series of separating orifices 7, 8 is preferably distributed over the entire circumference of the first separating wall 5, the second series of separating orifices 9 being distributed over the entire circumference of the second separating wall 6 .
  • the separation orifices 7, 8 of the first series of separation orifices 7, 8 are distributed over the first separation wall 5 according to a first staggered mesh, the separation orifices 9 of the second series of separation orifices 9 being distributed over the second separation wall 6 according to a second staggered mesh.
  • the separation orifices 7, 8, 9 are arranged both in a first helix and a second crossed helix, which improves the efficiency of sorting during the circulation of waste in the first trommel section 3 and in the second trommel section 4, regardless of the direction of rotation of said trommel sections 3, 4.
  • the first dividing wall 5 and/or the second dividing wall 6 is provided with lifting fins 22 for the waste circulating in the first trommel section 3 and/or in the second trommel section 4, respectively.
  • the lifting fins 22 are preferably each arranged in the longitudinal direction of the trommel sections 3, 4, so as to entrain, raise and stir the waste during the rotation of said trommel sections 3, 4.
  • the lifting fins 22 are advantageously staggered.
  • the first trommel section 3 and the second trommel section 4 form a single trommel 3, 4 rotatable in one piece around a single longitudinal axis X-X'-Y-Y', the output end of the first trommel section 3 being directly connected to the inlet end of the second trommel section 4.
  • the trommel sections 3, 4 are integral, and form a single drum.
  • the sorting machine 1 comprises three load bearings 23 making it possible to support and/or drive the single trommel in rotation, two of the load bearings 23 being placed at the ends of the single trommel, the last being placed roughly median to the other two.
  • the force pick-ups 23 correspond for example to bearings, and/or to drive means of the cogwheel or drive pulley type.
  • the median force absorption 23 advantageously makes it possible to avoid any risk of bending of the single trommel 3, 4, in particular in the case where its total length is significant and where the quantity of waste within it is particularly massive.
  • the sorting machine 1 including means for transferring the second residual fraction of waste 14 from the first section of trommel 3 to the second trommel section 4.
  • the first trommel section 3 preferably comprises a transfer outlet for the second residual fraction of waste 14, the second trommel section 4 comprising a secondary inlet for the second residual fraction of waste 14.
  • the secondary inlet is advantageously connected to the transfer outlet, so that the waste can circulate from the first trommel section 3 to the second trommel section 4.
  • the sorting machine 1 is designed so that the second residual fraction of waste 14 falls by gravity from the first trommel section 3 into the second trommel section 4.
  • fractions and sub-fractions of waste 13, 15, 18 recovered separately in the hoppers 12, 17, 18 can thus be treated separately, despite the very great heterogeneity of the initial mixture of waste 2.
  • the treatment installation also comprises a composting installation making it possible to subject the first fraction of waste 13 to a composting process so as to compost at least in part the biodegradable waste that it contains.
  • the composting installation advantageously makes it possible to implement step E2 described above. Consequently, the elements of this composting installation, and in particular the first composting bay 3C, the second composting bay 3C, the drying bay 2C, the separation means, advantageously correspond to those described above.
  • the first bay, and/or the second bay comprise sources of humidity 6C making it possible to moisten the mixture of waste 2 concerned, that is to say respectively the first fraction of waste 13 and the portion of 13C light waste.
  • the drying bay 2C comprises a recuperator 10C of a portion of the humidity 6C contained in the mixture of pre-composted waste 2 during the drying of the latter, the recuperator 10C making it possible to supply the sources of 6C humidity with the 6C humidity recovered during the drying of said pre-composted waste.
  • the recuperator 10C advantageously corresponds to that described above, and comprises for example a device for condensing the humidity 6C contained in the drying air, which has been extracted from the mixture of pre-composted waste 2.
  • the recuperator 10C also includes, for example, a device for draining the composting juices 11C, arranged at ground level 12D, making it possible to capture and drain said composting juices 11C.
  • Such an arrangement advantageously makes it possible to create a circulation of drying air A dry from top to bottom suitable for allowing the mixture of pre-composted waste 2 to be dried.
  • the condensation device is preferably placed within the suction means 8C and/or the blowing means 7C.
  • the drying bay 2C preferably comprises a light source 5C as described above, making it possible to irradiate the mixture of waste 2 during drying, and thus facilitate its drying.
  • the composting bay 3C advantageously also comprises a light source 5C making it possible to irradiate the mixture of waste 2 during composting, and thus to improve the composting of the latter (as illustrated in figure 9 ), natural light, and in particular the sun's rays being conducive to the development of life, and in particular to the micro-organisms which are sensitive to it.
  • the light source 5C can advantageously be formed by a canopy placed directly above the composting bay 3C or the drying bay 2C, allowing sunlight to pass through and protecting the bay from bad weather.
  • the composting installation also advantageously comprises means for treating the drying air A dry having circulated through the mixture of pre-composted waste 2 to discharge it substantially from any composting emission, in particular odorous, as described for example above.
  • the composting bays and the drying bays are identical, and/or are combined, to form composting/drying bays and selectively provide the two associated functions.
  • the drying bays and the composting bays can be perfectly distinct without departing from the scope of the invention.
  • the separation means preferably include at least one ballistic carpet separator 12C and an associated densimetric table separator making it possible to separate the portion of heavy waste 25 and the portion of light waste 13C.
  • the installation advantageously comprises means for adding (not shown), to the second residual fraction of waste 14, the portion of heavy waste 25 separated from the means of separation of the composting installation.
  • the means of addition can take the form, for example, of a conveyor designed to transport the portion of heavy waste 25 in order to add it to the second residual fraction of waste 14.
  • portion of heavy waste 25 recovered from the first fraction of waste 13 can thus advantageously be added to the second residual fraction of waste 14 at the end of step E1.
  • the processing installation comprises at least one line for automatic sorting of waste from a sub-fraction of small waste 15 from the second residual fraction of waste 14 (preferably associated with step E6), and at least a line for manual sorting of a large waste sub-fraction of the second residual waste fraction 14 (preferably associated with step E5), the large waste sub-fraction being formed by waste whose size is greater to the sub-fraction of small waste (15), the sorting lines making it possible to separate recyclable waste (26) from the second residual fraction of waste (14), as well as non-recyclable waste.
  • the automatic sorting line preferably includes a ballistic belt separator, an accelerator belt, a low recovery means, a high recovery means, a glass trap, a tungsten strip scraper, robots for sorting substantially flat waste, robots for sorting substantially voluminous waste, sets of belt conveyors.
  • the processing facility preferably comprises a facility for manufacturing solid recovered fuel from non-recyclable waste separated using sorting lines, making it possible in particular to perform step X described above.
  • the invention finds its industrial application in the design, production and implementation of means for processing a mixture of waste of heterogeneous sizes, shapes and consistencies, a mixture comprising biodegradable waste and non-biodegradable recyclable waste.

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Claims (11)

  1. Verfahren zur Behandlung eines Abfallgemisches (2), das aus Haushaltsabfällen und/oder gewerblichen Abfällen gebildet wird, die keiner vorherigen Sortierung unterzogen wurden, wobei es das Ziel ist, eine Trennung von biologisch abbaubaren Abfällen und recycelbaren, nicht biologisch abbaubaren Abfällen durchzuführen, wobei die Abfälle von heterogener Größe, Form und Konsistenz sind, wobei ein nicht vernachlässigbarer Anteil der Masse des Abfallgemisches (2) aus biologisch abbaubaren Abfällen gebildet wird, beispielsweise wenigstens 10 % der Masse, und wenigstens 20 % der Masse des Gemisches aus recycelbaren, nicht biologisch abbaubaren Abfällen (26) gebildet werden, wobei das Behandlungsverfahren die folgenden aufeinanderfolgenden Schritte umfasst:
    - Schritt E1, bei dem das Abfallgemisch (2) durch eine erste Reihe von Trennöffnungen (7, 8) in eine erste Abfallfraktion (13) mit einer Größe von weniger als etwa 180 mm, vorzugsweise weniger als 140 mm, und in eine restliche zweite Abfallfraktion (14) getrennt wird, wobei die erste Reihe von Trennöffnungen (7, 8) primäre Öffnungen (7) und sekundäre Öffnungen (8) umfasst, deren Größe größer ist als die Größe der primären Öffnungen (7), sodass das Abfallgemisch (2) zuerst mit den sekundären Öffnungen und anschließend mit den primären Öffnungen (7) in Kontakt gelangt,
    - Schritt E2, bei dem die erste Abfallfraktion (13) einem Kompostierungsprozess unterzogen wird, um die biologisch abbaubaren Abfälle, die sie enthält, wenigstens zum Teil zu kompostieren.
  2. Behandlungsverfahren nach Anspruch 1, dadurch gekennzeichnet, dass die sekundären Öffnungen (8) eine Größe aufweisen, die geeignet ist, den Durchgang von Abfällen zuzulassen, deren Größe zwischen dem 1-fachen und dem 1,5-fachen der Größe der Abfälle liegt, deren Durchgang durch die primären Öffnungen (7) zugelassen wird.
  3. Behandlungsverfahren nach einem der vorhergehenden Ansprüche, dadurch gekennzeichnet, dass die Abfälle der ersten Abfallfraktion (13) eine Größe von unter etwa 110 mm aufweisen.
  4. Behandlungsverfahren nach dem vorhergehenden Anspruch, dadurch gekennzeichnet, dass wenigstens 10 %, vorzugsweise wenigstens 20 % der Masse des Gemisches aus biologisch abbaubaren Abfällen gebildet werden.
  5. Behandlungsverfahren nach einem der vorhergehenden Ansprüche, dadurch gekennzeichnet, dass die Abfälle keiner vorherigen Zerkleinerung unterzogen wurden.
  6. Behandlungsverfahren nach einem der vorhergehenden Ansprüche, dadurch gekennzeichnet, dass es umfasst:
    - einen Schritt W, bei dem ein Recycling der recycelbaren, nicht biologisch abbaubaren Abfälle (26), die beim Schritt E2 vorher von der ersten Abfallfraktion (13) getrennt wurden, und der recycelbaren Abfälle (26), die vorher von der restlichen zweiten Abfallfraktion (14) getrennt wurden, durchgeführt wird, und
    - einen Schritt X, bei dem vorzugsweise nicht recycelbare Abfälle (27), die im Schritt E2 von der ersten Abfallfraktion (13) getrennt wurden und die von der restlichen zweiten Abfallfraktion (14) getrennt wurden, zur Wiederverwertung einem Prozess der Herstellung von festen Brennstoffen unterzogen werden.
  7. Behandlungsverfahren nach einem der vorhergehenden Ansprüche, dadurch gekennzeichnet, dass es nach dem Schritt E1 oder gleichzeitig mit diesem einen Schritt E4 zur Trennung der restlichen zweiten Abfallfraktion (14) in eine Unterfraktion grober Abfälle und eine Unterfraktion kleiner Abfälle (15) umfasst, wobei die Unterfraktion grober Abfälle aus Abfällen gebildet wird, deren Größe größer ist als jene der Unterfraktion kleiner Abfälle (15).
  8. Behandlungsverfahren nach dem vorhergehenden Anspruch, dadurch gekennzeichnet, dass die Unterfraktion grober Abfälle aus Abfällen mit einer Größe von mehr als etwa 330 mm gebildet wird und die Unterfraktion kleiner Abfälle (15) aus Abfällen mit einer Größe von weniger als etwa 330 mm gebildet wird.
  9. Behandlungsverfahren nach einem der Ansprüche 7 oder 8, dadurch gekennzeichnet, dass es einen Schritt E5 der manuellen Sortierung der Unterfraktion grober Abfälle umfasst, der es ermöglicht, einerseits die in ihr enthaltenen recycelbaren Abfälle (26) und andererseits die in ihr enthaltenen nicht recycelbaren Abfälle (27) zu trennen.
  10. Behandlungsverfahren nach einem der Ansprüche 7 bis 9, dadurch gekennzeichnet, dass es einen Schritt E6 der automatisierten Sortierung der Unterfraktion kleiner Abfälle (15) umfasst, der es ermöglicht, einerseits die in ihr enthaltenen recycelbaren Abfälle (26) und andererseits die in ihr enthaltenen nicht recycelbaren Abfälle (27) zu trennen.
  11. Behandlungsverfahren nach einem der vorhergehenden Ansprüche, dadurch gekennzeichnet, dass das Verfahren vor dem Schritt E1 einen Schritt E7 des Öffnens von Säcken (24) des Typs Müllsäcke aus Kunststoff umfasst, wobei in diesen Säcken (24) das Abfallgemisch (2) enthalten ist, um das Abfallgemisch (2) aus den Säcken (24) freizugeben, um den Schritt E1 auszuführen.
EP15732793.3A 2014-05-23 2015-05-22 Verfahren zur behandlung eines abfallgemisches, einschliesslich trennung und kompostierung des besagten gemisches Active EP3145898B1 (de)

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Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11064647B2 (en) * 2016-04-09 2021-07-20 Mike Altomare Robotic litter processing system
CN107876371A (zh) * 2017-12-05 2018-04-06 江西悦丰农业科技有限公司 一种带旋转钢丝刷的圆筒网筛
US20220184855A1 (en) 2020-12-14 2022-06-16 Anellotech, Inc. Robotic separation of plastics for chemical recycling
US20230048485A1 (en) * 2021-08-11 2023-02-16 Atlas Organics, LLC Non-organic contamination removal automation process
US11998953B2 (en) * 2021-11-05 2024-06-04 Republic Services Intellectual Property Holdings, Llc Recovery of higher volume and higher quality recyclables from a mixed stream
JP7167373B1 (ja) 2022-02-14 2022-11-08 株式会社潮来工機 焼却灰の処理方法及び焼却灰の処理装置、並びに製鋼原料

Family Cites Families (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ES518876A0 (es) * 1983-01-10 1984-08-01 Enrique Carbonell Serra Proceso para el tratamiento de residuos urbanos e instalacion para su realizacion
JPS60161777A (ja) * 1984-01-31 1985-08-23 株式会社荏原製作所 乾電池分別装置
DE3916866A1 (de) * 1988-06-09 1990-11-29 Artur Richard Greul Verfahren zur fraktionierenden konditionierung von hausmuell etc.
US5071075A (en) * 1988-07-18 1991-12-10 Wiens Thomas J Solid waste disposal
US5250100A (en) * 1989-02-06 1993-10-05 World Life Resource, Inc. Solid waste recovery system
US5009370A (en) * 1989-05-11 1991-04-23 New Life Foundation Municipal solid waste material sorting trommel system
FR2668398B1 (fr) * 1990-10-25 1992-12-24 Otv D Procede et dispositif pour extraire la matiere organique contenue dans les dechets menagers.
ES2190549T3 (es) * 1996-10-21 2003-08-01 Herhof Umwelttechnik Gmbh Procedimiento para la separacion de una mezcla de residuos.
DE19803140A1 (de) * 1998-01-28 1999-07-29 Zweckverband Abfallbeseitigung Verfahren sowie Vorrichtung zur Durchführung des Verfahrens zur stofflichen Verwertung von Resthausabfällen
KR100351733B1 (ko) * 2000-03-21 2002-09-05 김구회 2단 역회전 매립토사 쓰레기 선별장치
JP2002138281A (ja) * 2000-11-02 2002-05-14 Kawasaki Steel Corp ごみ固形燃料から作製した土壌改良材
RU2209693C1 (ru) * 2001-11-26 2003-08-10 Армашевский Владимир Владимирович Способ переработки бытовых отходов
US8809038B1 (en) * 2003-04-30 2014-08-19 Recology Inc. Process for treatment of organic waste materials
ITMI20052430A1 (it) * 2005-12-21 2007-06-22 Sorain Cecchini Ambiente Sca S P A Nessuna
AU2007219618A1 (en) * 2006-03-02 2007-09-07 Conporec Inc. Composting apparatus, installation and method thereof
US7955839B2 (en) * 2006-06-23 2011-06-07 Recology Inc. Systems and methods for converting organic waste materials into useful products
FR2951095B1 (fr) * 2009-10-09 2012-10-05 Suez Environnement Procede et installation de traitement de dechets menagers, et autres dechets assimiles
FR2956990B1 (fr) * 2010-03-08 2012-04-20 Vinci Environnement Procede et dispositif de traitement des produits lourds issus d'un affinage de dechets provenant d'un traitement biologique.
FR2988625B1 (fr) * 2012-03-27 2014-04-18 Sita France Procede pour le traitement de dechets, notamment d'ordures menageres, et installation pour mettre en oeuvre ce procede
CN102671928B (zh) * 2012-05-07 2014-02-26 四川川润环保能源科技有限公司 一种城市混合垃圾分选及综合利用方法

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RU2016148700A3 (de) 2018-10-03
CY1125160T1 (el) 2024-02-16
CU24500B1 (es) 2021-04-07
CA2949917A1 (en) 2015-11-26
KR20170010837A (ko) 2017-02-01
BR112016027407A2 (pt) 2021-08-17
EP3145898A1 (de) 2017-03-29
SA516380368B1 (ar) 2020-12-21
PH12016502328A1 (en) 2017-02-06
SG11201609808XA (en) 2016-12-29
ES2912893T3 (es) 2022-05-30
CU20160175A7 (es) 2017-06-05
MA39544B2 (fr) 2021-01-29
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AU2015263137A1 (en) 2017-01-05
US20170158574A1 (en) 2017-06-08
CA2949917C (en) 2022-08-02
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MY179843A (en) 2020-11-18
KR102496359B1 (ko) 2023-02-03
PH12016502328B1 (en) 2017-02-06
FR3021238A1 (fr) 2015-11-27
DOP2016000303A (es) 2017-02-15
NZ727152A (en) 2021-03-26
DK3145898T3 (da) 2022-05-09
FR3021238B1 (fr) 2020-07-03
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AU2015263137B2 (en) 2020-01-30
MA39544A1 (fr) 2017-06-30

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